scholarly journals Zeolites and related sorbents with narrow pores for CO2 separation from flue gas

RSC Advances ◽  
2014 ◽  
Vol 4 (28) ◽  
pp. 14480-14494 ◽  
Author(s):  
Ocean Cheung ◽  
Niklas Hedin
Keyword(s):  
Carbon Dioxide ◽  
Flue Gas ◽  
Co2 Separation ◽  
Emission Sources

Adsorbents with small pores are especially relevant for capturing carbon dioxide at large emission sources.

Analysis of the Flue Gas Preparation Process for the Purposes of Carbon Dioxide Separation Using the Adsorption Methods

2017 ◽  
Vol 140 (3) ◽  
Author(s):  
Robert Zarzycki ◽  
Marcin Panowski
Keyword(s):  
Carbon Dioxide ◽  
Energy Expenditure ◽  
Flue Gas ◽  
Carbon Dioxide Emissions ◽  
Low Energy ◽  
Co2 Separation ◽  
Gas Temperature ◽  
Separation Unit ◽  
Carbon Dioxide Separation ◽  
Characteristic Features

The necessity of limitation of carbon dioxide emissions, which also concerns the energy sector, causes that more and more effective and efficient methods of CO2 capture from the flue gas are being tested. Among these technologies are adsorption ones, which have been used for a gas separation for many years. The characteristic features of adsorption separation are: long life of the sorbents used, low energy expenditure, and minim effect on the environment; however, their application requires adequate initial preparation of the flue gas fed into the system of CO2 separation so that the flue gas temperature is as low as possible, and there is no water content in it. The study presents the concept and numerical calculations of the system for preparation of the flue gas feeding the CO2 adsorption (vacuum pressure swing adsorption (VPSA)) separation unit, using the absorption chiller (AC). In the presented concept, the AC is driven by the flue gas which is used as both: upper and lower heat source for AC; however, due to the amount of energy being carried out with the flue gas, which is larger than required by the AC, the additional heat exchangers must be implemented. The calculations presented in the study show that owing to the application of AC, flue gas may be cooled down to temperatures even about 5 °C. Moreover, the simultaneous process of flue gas cooling and drying in such system is realized at low energy expenditure which leads to improvement of the overall energy efficiency of the system of CO2 separation from flue gas and also to reduction of its dimensions.

Application of Disk Aerators to Recarbonation of Alkaline Wastewater from Wet Gasification of Carbide

1991 ◽  
Vol 24 (7) ◽  
pp. 277-284 ◽  
Author(s):  
E. Gomólka ◽  
B. Gomólka
Keyword(s):  
Carbon Dioxide ◽  
Liquid Phase ◽  
Gas Phase ◽  
Flue Gas ◽  
Carbonic Acid ◽  
Low Cost ◽  
Flue Gases ◽  
Carbon Dioxide Content ◽  
Patent Claim ◽  
Phase Dispersion

Whenever possible, neutralization of alkaline wastewater should involve low-cost acid. It is conventional to make use of carbonic acid produced via the reaction of carbon dioxide (contained in flue gases) with water according to the following equation: Carbon dioxide content in the flue gas stream varies from 10% to 15%. The flue gas stream may either be passed to the wastewater contained in the recarbonizers, or. enter the scrubbers (which are continually sprayed with wastewater) from the bottom in oountercurrent. The reactors, in which recarbonation occurs, have the ability to expand the contact surface between gaseous and liquid phase. This can be achieved by gas phase dispersion in the liquid phase (bubbling), by liquid phase dispersion in the gas phase (spraying), or by bubbling and spraying, and mixing. These concurrent operations are carried out during motion of the disk aerator (which is a patent claim). The authors describe the functioning of the disk aerator, the composition of the wastewater produced during wet gasification of carbide, the chemistry of recarbonation and decarbonation, and the concept of applying the disk aerator so as to make the wastewater fit for reuse (after suitable neutralization) as feeding water in acetylene generators.

Carbon dioxide capture from a real coal-fired flue gas using K-based solid sorbents in a 0.5 MWe-scale test-bed facility

2020 ◽  
Vol 103 ◽  
pp. 103192
Author(s):  
Young Cheol Park ◽  
Sung-Ho Jo ◽  
Jae-Young Kim ◽  
Yooseob Won ◽  
Hyungseok Nam ◽  
...  
Keyword(s):  
Carbon Dioxide ◽  
Flue Gas ◽  
Carbon Dioxide Capture ◽  
Test Bed ◽  
Solid Sorbents ◽  
Scale Test

Biological elimination of nitric oxide and carbon dioxide from flue gas by marine microalga NOA-113 cultivated in a long tubular photobioreactor

1996 ◽  
Vol 82 (4) ◽  
pp. 351-354 ◽  
Author(s):  
Ken-Ichi Yoshihara ◽  
Hiroyasu Nagase ◽  
Kaoru Eguchi ◽  
Kazumasa Hirata ◽  
Kazuhisa Miyamoto
Keyword(s):  
Nitric Oxide ◽  
Carbon Dioxide ◽  
Flue Gas ◽  
Tubular Photobioreactor ◽  
Marine Microalga

The role of Tween 80 and SDS in the kinetics of semi-clathrate hydrates formation for carbon dioxide capture from flue gas

2021 ◽  
pp. 1-15
Author(s):  
Anton Petukhov ◽  
Artem Atlaskin ◽  
Maria Sergeeva ◽  
Sergey Kryuchkov ◽  
Dmitry Shablykin ◽  
...  
Keyword(s):  
Carbon Dioxide ◽  
Flue Gas ◽  
Carbon Dioxide Capture ◽  
Tween 80 ◽  
Clathrate Hydrates ◽  
Kinetics Of

High Flue Gas Flow Rate Tests for Removal and Recovery of Carbon Dioxide under Power Plant Effluent Gas Conditions

2004 ◽  
Vol 30 (6) ◽  
pp. 758-761
Author(s):  
Tomio MIMURA ◽  
Yasuyuki YAGI ◽  
Masaki IIJIMA ◽  
Ryuji YOSIYAMA ◽  
Takahito YONEKAWA
Keyword(s):  
Carbon Dioxide ◽  
Power Plant ◽  
Flow Rate ◽  
Flue Gas ◽  
Gas Flow ◽  
Gas Flow Rate ◽  
Power Plant Effluent ◽  
Removal And Recovery

Adaptive evolution and carbon dioxide fixation of Chlorella sp. in simulated flue gas

2019 ◽  
Vol 650 ◽  
pp. 2931-2938 ◽  
Author(s):  
Dujia Cheng ◽  
Xuyang Li ◽  
Yizhong Yuan ◽  
Chengyu Yang ◽  
Tao Tang ◽  
...  
Keyword(s):  
Carbon Dioxide ◽  
Adaptive Evolution ◽  
Flue Gas ◽  
Carbon Dioxide Fixation ◽  
Chlorella Sp
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